ref: letter – 25 june 2008 p0106-02 · 2013-07-26 · ref: letter – 25 june 2008 p0106-02 page...
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 1 of 47
1. Oil Interceptor - Classification of oil interceptors There are 4 Interceptors on the surface water drainage lines at the facility marked as INT on
the attached Site Surface Water Layout Drawing (Attachment A: D100/001). The
interceptors are located on the discharge from the licensed discharge points SW1 and SW2
and also at a location upstream of SW1 and on SW3 discharge point. While the detailed
design specifications were not found in the archives from the installation date of 1995-1996,
information sourced from the Consulting Engineers who assisted with the specifications was
obtained. From this information, the main interceptors on SW1 and SW2 are three chamber
Class 1 Petrol Interceptors each of capacity 5000litres.
The area served by a Class 2 Interceptor (SW3) is a concrete surfaced area at the rear of the
Metal Parts Building. There is no potential for significant contamination of surface water in
this area because, aside from incoming materials, the area is used only for storage of empty
transformers and scrap metal. Although incoming deliveries are routed across this area,
vehicles do not routinely park there and do not remain for extended time periods.
ENVA – Formerly Atlas Oils is engaged twice a year to clean out the interceptors and they
agree with this conclusion. The design specification sourced from Garland Engineers is
attached for information – Attachment B SK-1
Location of Interceptor Class Located in the back yard - #1
Class 1 – Three chambers
Located in the back yard - #2
Class 2 – One chamber
Prior to emission to SW-1 -#3
Class 1 – Three chambers
Prior to emission to SW-2 - #4
Class 1 – Three chambers
Reference attached drawings
� D100/001 detailing the location of the oil interceptors on-site – Attachment A
� Drawing Number SK-1, detailing the type of interceptor used – Attachment B
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EPA Export 26-07-2013:02:39:09
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 2 of 47
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EPA Export 26-07-2013:02:39:09
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 3 of 47
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Ref: Letter – 25 June 2008 P0106-02
Page 4 of 47
2. Update to Trade Effluent Sewer to include SE-2 Reference attached drawing:
� D100/001 highlighting the location of the SE-2 – Attachment C & Attachment D
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 5 of 47
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 6 of 47
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 7 of 47
3. Emissions to Air - Emissions to Atmosphere from E-Coat process The painting process consists of 3 stages – Pre-Treatment, E-Coat and Powder Coat. The Pre-Treatment stage involves immersion of parts in baths
containing surfactant cleaning solutions, alkaline cleaners, water and a phosphating solution. The temperature of the baths is at ambient (unheated) to a
maximum of 65-75oC (Alkaline Cleaner Bath) and 45-55oC (Zinc Phosphate Bath). The E-Coat stage consists of immersion of parts in an E–Coat
solution at 30oC followed by water rinses and then drying of parts in the Stoving/Curing Oven. An extract system collects water vapour for discharge
above the level of the roof via 3 flues. The emissions from the Stoving/Curing Oven are released through Emission Points A26A, A26B, A26C and these
emissions are monitored annually. Emissions from the Powder Coat Oven (A27A, A27B) are also monitored annually. The emissions from the Pre-
Treatment and part of the E-Coat Stage of the paint process are not significant. The chemical composition of the solutions was reviewed and due to the
non-volatile constituents as well as low temperatures, emissions would not contain harmful constituents.
E-Coating Process
Tank Treatment3 Areas
1.Pre-Treatment
2.E-Coating
3.Powder Coating
Coating electrically deposited onto the surface
of the steel and rinsed
Stage 11: E-coat analyte
Consituents listed:Demin waterEC-solvent: 2-(2-butoxyethoxy ethanol 100%, Solvent : 2-butoxyethanol 49.5%Pigment pasteEC3000 Resin Aqua EC2000/3000Neutralizing agent: Acetic acid 50%Anti-crater agent: formic acid 1.7%, 1-methoxy2-propanol 1.3%Edge protection agent: 2-butoxyethanol, 1-methoxy-2-propanolThickness additive: butanol 50%, sec-butanol 50%
Stage 12: UltrafiltrationStage 13: UltrafiltrationStage 14: Ultrafiltration
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Ref: Letter – 25 June 2008 P0106-02
Page 8 of 47
3. Emissions to Air - Emissions to Atmosphere from E-Coat process contd: Diagram of the Stoving (E-coat) and Curing (Powder coat) oven – emission points labelled:
POWDEROVEN
E-COATOVEN
Oven ExhaustA27A
Oven ExhaustA26A
ENTRY OVEN EXHAUST(Common To Both Ovens)A27B
ENTRY OVEN EXHAUST(Common To Both Ovens)A26B
AIR SEAL TO ATMOSPHEREA26CSTAIRS STAIRS
OVENENTRY &EXIT THISEND
A27A
A26A
A27B
A26B A26C
AUTOFINORGINALISSUE
OVEN EXHAUST POSITIONS
PAUWELS TRAFO
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Ref: Letter – 25 June 2008 P0106-02
Page 9 of 47
4. Table E.1 (i) for all boiler emissions
Emission Point: Emission Point Ref. No:
A21
Location:
AP Building Domestic Boiler
Grid Ref. (12 digit, 6E,6N):
243706E, 304218N
Vent Details
Diameter: 0.15m
Height above Ground(m): 1m
Date of commencement of emission:
1977
Characteristics of Emission:
Boiler rating Steam Output: Thermal Input:
N/A kg/hr
MW Boiler fuel Type: Maximum rate at which fuel is burned % sulphur content:
Oil kg/hr < 1% S
NOx 300 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel) Maximum volume* of emission
2000 m3/hr 0oC, 3 % O2 (liquid or gas), 6 % O2 (solid fuel)
Temperature
236oC(max) 180oC(min) 200oC(avg)
* Volume flow limits for emissions to atmosphere shall be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa), dry gas; 3% oxygen for liquid and gas fuels; 6% oxygen for solid fuels. (i) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up/shutdown to be included): Periods of Emission (avg) 60 min/hr 12 hr/day 120 day/yr
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Ref: Letter – 25 June 2008 P0106-02
Page 10 of 47
Table E.1 (i) BOILER EMISSIONS TO ATMOSPHERE (1 Page for each emission point) Emission Point: Emission Point Ref. No:
A22
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
-
Vent Details
Diameter: 0.2m
Height above Ground(m): 3
Date of commencement of emission:
1992
Characteristics of Emission:
Boiler rating Steam Output: Thermal Input:
kg/hr MW
Boiler fuel Type: Maximum rate at which fuel is burned % sulphur content:
OIL
kg/hr < 1% S
NOx 100mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel) Maximum volume* of emission
500m3/hr 0oC, 3 % O2 (liquid or gas), 6 % O2 (solid fuel)
Temperature
180oC(max) 140oC(min) 170oC(avg)
* Volume flow limits for emissions to atmosphere shall be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa), dry gas; 3% oxygen for liquid and gas fuels; 6% oxygen for solid fuels. (i) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up/shutdown to be included): Periods of Emission (avg) 60 min/hr 12 hr/day 120 day/yr
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 11 of 47
Table E.1 (i) BOILER EMISSIONS TO ATMOSPHERE (1 Page for each emission point) Emission Point:
Emission Point Ref. No:
A30
Location:
Archives Building, Canteen Boiler
Grid Ref. (12 digit, 6E,6N):
Vent Details
Diameter: 0.11
Height above Ground(m): 3
Date of commencement of emission:
2004
Characteristics of Emission:
Boiler rating Steam Output: Thermal Input:
kg/hr
0.025 MW Boiler fuel Type: Maximum rate at which fuel is burned % sulphur content:
GAS kg/hr
< 0.2% S NOx < 160 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel) Maximum volume* of emission
m3/hr < 3 0oC, 3 % O2 (liquid or gas), 6 % O2 (solid fuel)
Temperature
80oC(max) 60oC(min) 70oC(avg)
* Volume flow limits for emissions to atmosphere shall be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa), dry gas; 3% oxygen for liquid and gas fuels; 6% oxygen for solid fuels. (i) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up/shutdown to be included): Periods of Emission (avg) 60 min/hr 12 hr/day 120 day/yr
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Ref: Letter – 25 June 2008 P0106-02
Page 12 of 47
5. Status of Emission point A15 Emission point A15 (Final Spray Exhaust) was dismantled completely in April 2008. The booth
was very infrequently used. From our previous Annual Environmental Report submissions you will
have noted the Final Spray Exhaust (A15) was not operational during annual monitoring only once
since 2002. The paint waste was removed stored in barrels and is currently awaiting Hazardous
waste disposal.
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Ref: Letter – 25 June 2008 P0106-02
Page 13 of 47
6. Emissions to Air – Table E.1(ii) and E.1(iii)
TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A4A
Source of Emission:
Shotblast
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243856E, 304198N
Vent Details Diameter:
Height above Ground(m):
0.5m 11m
Date of commencement:
1987
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 136,000 Nm3/d Maximum/day 136,000 Nm3/d
Maximum rate/hour 8,500 Nm3/h Min efflux velocity 5 m.sec-1
(ii) Other factors
Temperature 25oC(max) oC(min) 20oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 40 min/hr 16 hr/day 220 day/yr
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Ref: Letter – 25 June 2008 P0106-02
Page 14 of 47
TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemica l characteristics of the emission (1 table per emission point) Emission Point Reference Number: A4A Old Shotblast
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Particulate 20 50 0.16 1.5 Reverse Jet Cleaning Cartridge 5 10 0.04 0.08 141 282
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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Page 15 of 47
TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A4B
Source of Emission:
New Shotblast
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243876E, 304221N
Vent Details Diameter:
Height above Ground(m):
0.3m 11m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 179,520 Nm3/d Maximum/day 272,000 Nm3/d
Maximum rate/hour 17,000 Nm3/h Min efflux velocity 5 m.sec-1
(ii) Other factors
Temperature 25oC(max) oC(min) 20oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 40 min/hr 16 hr/day 220 day/yr
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Page 16 of 47
TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A4B New Shotblast
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Particulate 20 50 0.34 0.85 Reverse Jet Cleaning Cartridge 5 10 0.085 0.170 299.2 598.4
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 17 of 47
TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A29
Source of Emission:
New Drying Oven
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243747E, 304139N
Vent Details Diameter:
Height above Ground(m):
0.3m 11.5m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 240,000 Nm3/d Maximum/day 240,000 Nm3/d
Maximum rate/hour 10,000 Nm3/h Min efflux velocity 4 m.sec-1
(ii) Other factors
Temperature 200oC(max) oC(min) 150oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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Page 18 of 47
TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A29 New Drying Oven_________
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Organics None 2 10 0.02 0.10 105.6 528
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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Page 19 of 47
TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A26A
Source of Emission:
Stoving / E-Coat Oven
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243909E, 304176E
Vent Details Diameter:
Height above Ground(m):
0.4 10m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 240,000 Nm3/d Maximum/day 240,000 Nm3/d
Maximum rate/hour 10,000 Nm3/h Min efflux velocity 4 m.sec-1
(ii) Other factors
Temperature 200oC(max) oC(min) 150oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical cha racteristics of the emission (1 table per emission point) Emission Point Reference Number: A26A Stoving / E-Coat Oven___
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Organics None 2 10 0.02 0.10 105.6 528
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A26B
Source of Emission:
Stoving / E-Coat Oven
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243919E, 304172N
Vent Details Diameter:
Height above Ground(m):
0.4m 10
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 240,000 Nm3/d Maximum/day 240,000 Nm3/d
Maximum rate/hour 10,000 Nm3/h Min efflux velocity 4m.sec-1
(ii) Other factors
Temperature 200oC(max) oC(min) 150oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A26B Stoving / E-Coat Oven
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Organics None 2 10 0.02 0.10 105.6 528
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A26C
Source of Emission:
Stoving / E-Coat Oven
Location:
Powder Oven
Grid Ref. (12 digit, 6E,6N):
243921E, 304171N
Vent Details Diameter:
Height above Ground(m):
0.3m 10m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 240,000 Nm3/d Maximum/day 240,000 Nm3/d
Maximum rate/hour 10,000 Nm3/h Min efflux velocity 5 m.sec-1
(ii) Other factors
Temperature 250oC(max) oC(min) 180oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A26C Stoving / E-Coat Oven
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Organics None 5 10 0.05 0.10 264 528
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A27A
Source of Emission:
Curing / Powder Oven
Location:
Powder Oven
Grid Ref. (12 digit, 6E,6N):
243903E, 304174N
Vent Details Diameter:
Height above Ground(m):
0.3m 10m
Date of commencement:
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 240,000 Nm3/d Maximum/day 240,000 Nm3/d
Maximum rate/hour 10,000 Nm3/h Min efflux velocity 5 m.sec-1
(ii) Other factors
Temperature 250oC(max) oC(min) 180oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A27A Curing / Powder Oven
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Organics None 5 10 0.05 0.10 264 528
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A27B
Source of Emission:
Curing / Powder Oven
Location:
Tanking Area
Grid Ref. (12 digit, 6E,6N):
243920E, 304176N
Vent Details Diameter:
Height above Ground(m):
0.18m 10m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 192,000 Nm3/d Maximum/day 192,000 Nm3/d
Maximum rate/hour 8,000 Nm3/h Min efflux velocity 5 m.sec-1
(ii) Other factors
Temperature 250oC(max) oC(min) 100oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ________%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical c haracteristics of the emission (1 table per emission point) Emission Point Reference Number: A27B Curing / Powder Oven
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
SO2
NOx
CO
None
None
None
1.75
8.1
123
4.5
100
406
0.014
0.065
0.985
0.036
0.160
3.25
73.9
343
5200
190
845
17160
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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7. Emissions to Air – Classification of Emission Points
Emissions to atmosphere from all emission sources are monitored annually. Monitoring reports
from 2000-2007 have been reviewed and the data shows that emission levels are consistently at or
below the limit of detection for most parameters on most occasions. The BAT Guidance Note for
Non Ferrous Metals and Galvanising gives guidance on the expected BAT emission levels for all
parameters which are monitored and the levels are consistently below the BAT level and are
typically less than 10-20% of the relevant BAT Limit. It is therefore reasonable to classify all of the
emission points as Minor Emission Points. The Guidance Note suggests that when abatement
systems are installed that the emissions should be considered as Major Emission Points. The two
Shotblasts (Emission Points A4A and A4B) have Reverse Jet Cleaning Systems fitted to collect
dust from the shotblasting apparatus. Review of monitoring data for these emission points for 2000-
2007 suggests that the emissions from the systems are always significantly lower than the BAT
Guidance levels. It is therefore our opinion that these two emission points should also be classified
as Minor Emission Points.
8. Emissions to Air – Abatement system on A4B
The abatement system installed in the New Shotblast (Emission Point A4B) is a Reverse Jet Filter
Cleaning System. Dust collected in the system is collected in a sealed drum under the unit. The
same type of abatement system is installed on the Old Shotblast (Emission Point A4B). There are 9
and 20 filter cartridges installed in the abatement units at Emission Points A4A and A4B,
respectively.
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TABLE F.1(i): ABATEMENT / TREATMENT CONTROL Emission point reference number : A4A Shotblast ______
Control1 parameter Equipment 2 Equipment maintenance Equipment calibration Equipment back-up
Pressure Differential Pressure Gauge Cleaning Annual
Control1 parameter Monitoring to be carried out3 Monitoring equipment Monitoring equipment calibration
Differential Pressure Continuous Differential Pressure Gauge Annual
1 List the operating parameters of the treatment / abatement system which control its function. 2 List the equipment necessary for the proper function of the abatement / treatment system. 3 List the monitoring of the control parameter to be carried out.
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TABLE F.1(i): ABATEMENT / TREATMENT CONTROL Emission point reference number : A4B New Shotblast
Control1 parameter Equipment 2 Equipment maintenance Equipment calibration Equipment back-up
Pressure Differential Pressure Gauge Cleaning Annual -
Control1 parameter Monitoring to be carried out3 Monitoring equipment Monitoring equipment calibration
Differential Pressure Continuous Differential Pressure Gauge Annual
1 List the operating parameters of the treatment / abatement system which control its function. 2 List the equipment necessary for the proper function of the abatement / treatment system. 3 List the monitoring of the control parameter to be carried out.
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9. Burn-off oven – Description of process This is a very simple process, non-conforming parts which have passed through the paint
system are introduced manually. It is important to reach a high temperature in order to
remove the paint, thus the temperature is continuously monitored during operation. A copy
of the specification of the burners used is attached – Attachment D. The emissions are not
abated and concentration of substances present are low. The emissions are minor as is
evident from previous monitoring data.
10. Treatment in the Burn-off Oven
The primary purpose of the Burn-off oven is to remove powder paint. The Powder painted
tanks and paint system load bars which are incorrect i.e. powder not aesthetically correct,
parts missing from the tank etc are ‘burned-off’. The oven is gas-fired thus some
combustion gas is emitted, which include Carbon Monoxide, Carbon Dioxide and Nitrogen
Oxides. All parts are 100% reused. The waste generated i.e. ash is collected in barrels and
disposed off.
11. Coating materials which undergo treatment in the burn-off oven
The non-conforming parts which undergo treatment in the Burn-off oven have passed
through the cleaning , zinc phosphating, E-coat and Powder coat processes. The parts have
also passed through the E-coat and Powder coat stoving oven and therefore the coating
materials are dry and solid. Therefore there are no volatile constituents remaining. A review
of all the materials used in the above processes was performed, the constituents remaining
on the parts prior to Burn-off were identified and are listed in the table below.
Process Stage Chemical Used (Constituents listed) Pre-treatment Conditioning rinse • Prepalene X - Zn3-phosphate 4H20 <25%.
Zinc Phosphate • Novaphos Z616 CMI- Phosphoric acid 10-20%,
Nickel nitrate - 5%max • Grenodine958 – Phosphoric acid 10-20%, Nickel
Nitrate 2-4%, Fluorosilicic acid 1-2% Electro-coat E-coat bath • Pigment pasteEC3000 –
• Resin Aqua EC2000/3000: Powder coating
Powder spray booths Auto & Manual
• Main constituent: Multi functional glicidyl esters 1-5%.
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12 Burn-off oven usage
Each ‘burn-off’ run is monitored using a chart recorder – this indicates the temperature and
time of each operation. During the previous calendar year i.e. 2007, the burn-off oven was
operational for a total of 234 hours (approximately 9.75 days). Normal usage is
approximately 8 hours per burn-off.
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13. Burn-off oven TABLE E.1(ii) MAIN EMISSIONS TO ATMOSPHERE (1 Page for each emission point)
Emission Point Ref. No:
A28
Source of Emission:
Burn Off Oven
Location:
Metal Parts Building
Grid Ref. (12 digit, 6E,6N):
243956E, 304217N
Vent Details Diameter:
Height above Ground(m):
0.11m 11m
Date of commencement:
1997
Characteristics of Emission:
(i) Volume to be emitted:
Average/day 16,000 Nm3/d Maximum/day 24,000 Nm3/d
Maximum rate/hour 1,000 Nm3/h Min efflux velocity 3 m.sec-1
(ii) Other factors
Temperature 850oC(max) oC(min) 800oC(avg)
For Combustion Sources: Volume terms expressed as : � wet. � dry. ___3____%O2
(iii) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up /shutdown to be included): Periods of Emission (avg) 60 min/hr 16 hr/day 220 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical ch aracteristics of the emission (1 table per emission point) Emission Point Reference Number: A28 Burn Off Oven
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Heavy Metals
HCL
Organics
None
None
None
0.08
2.5
2
0.22
8.5
5
7.7x10-5
0.0025
0.002
2.2x10-4
0.0085
0.005
0.407
13.2
10.6
1.16
44.9
26.4
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC,101.3kPa). Wet/dry should be the same as given in Table E.1(ii) unless clearly stated otherwise.
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TABLE F.1(i): ABATEMENT / TREATMENT CONTROL Emission point reference number : A28______
Control1 parameter Equipment 2 Equipment maintenance Equipment calibration Equipment back-up
Temperature Thermocouple
Recorded
Cleaning Annual
Control1 parameter Monitoring to be carried out3 Monitoring equipment Monitoring equipment calibration
Temperature Continuous Thermocouple
Recorded
Annual
1 List the operating parameters of the treatment / abatement system which control its function. 2 List the equipment necessary for the proper function of the abatement / treatment system. 3 List the monitoring of the control parameter to be carried out.
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14. Best Available Techniques (BAT) The Pauwels Trafo Ireland Ltd facility is subject to the requirements of the IPPC Directive and is
licenced by the EPA under the IPC/IPPC Licensing regime. Council Directive 96/61/EC on
integrated pollution prevention and control, the IPPC directive, defines a system of permitting for
certain types of activity. The purpose of the Directive is to achieve integrated prevention and
control of pollution arising from the activities listed in Annex I of the Directive, leading to a high
level of protection of the environment as a whole. The permits for activities listed in Annex I of the
IPPC Directive must be based on the concept of Best Available Techniques, or BAT, which is
defined in Article 2 of the IPPC Directive as follows:
“best available techniques shall mean the most effective and advanced stage in the development of
activities and their methods of operation which indicate the practical suitability of particular techniques
for providing in principle the basis for emission limit values designed to prevent and, where that is not
practicable, generally to reduce emissions and the impact on the environment as a whole”
“techniques shall include both the technology used and the way in which the installation is designed,
built, maintained, operated and decommissioned”
“available techniques shall mean those developed on a scale which allows implementation in the
relevant industrial sector, under economically and technically viable conditions, taking into
consideration the costs and advantages, whether or not the techniques are used or produced inside
the Member State in question, as long as they are reasonably accessible to the operator”.
'best` shall mean most effective in achieving a high general level of protection of the environment as
a whole.”
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14. Best Available Techniques (BAT) contd: In determining the best available techniques, the Directive specifies that special consideration must
be given to the items listed in Annex IV of the Directive as follows, “bearing in mind the likely
costs and benefits of a measure and the principles of precaution and prevention”:
1.the use of low-waste technology;
2.the use of less hazardous substances;
3.the furthering of recovery and recycling of substances generated and used in the process and of
waste, where appropriate;
4.comparable processes, facilities or methods of operation which have been tried with success on
an industrial scale;
5.technological advances and changes in scientific knowledge and understanding;
6.the nature, effects and volume of the emissions concerned;
7.the commissioning dates for new or existing installations;
8.the length of time needed to introduce the best available technique;
9.the consumption and nature of raw materials (including water) used in the process and their
energy efficiency;
10. the need to prevent or reduce to a minimum the overall impact of the emissions on the
environment and the risks to it;
11. the need to prevent accidents and to minimize the consequences for the environment;
12. the information published by the Commission pursuant to Article 16 (2) or by international
organizations.
The final decision on BAT rests with the Member State because Article 9 of the Directive
establishes that the licensing authority must take account of “the technical characteristics of the
installation concerned, its geographical location and the local environmental conditions”.
The Final Draft BAT Guidance Note on Best Available Techniques for Non-Ferrous Metals and
Galvanising is the relevant Guidance Note for the Pauwels Trafo facility. The Guidance Note
covers several sectors which includes “3.9 Boilermaking and the manufacture of reservoirs, tanks
and other sheet metal containers where the production area exceeds 500 square metres” which is
the Sector under which Pauwels Trafo are to be licenced. A review of site activities with specific
reference to this Guidance has been completed to ensure that Best Available Techniques are being
employed at the facility.
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14.1 BEST AVAILABLE TECHNIQUES (BAT) A SSESSMENT
14.1.1 Management Systems
Pauwels Trafo are accredited to ISO 14001 (2004) and have a strong Environmental Management System in
place. Environmental Policy Statement and commitment from Management to manage the environmental
impacts of the facility is a key feature of the system. As part of the Environmental Management System
Pauwels have implemented procedures to control the introduction of new products/new processes. These
procedures ensure approval from H&S, Environment and Quality departments prior to the implementation of
the change. They also ensure review of material specifications by our Design department and input from the
Engineering department where necessary.
14.1.2 Minimisation of Energy Use
Proactive Energy Management procedures are employed at the facility. Fans are switched off when not in
use, and regular reminders about energy conservation are issued to all personnel. One of the main projects
included in this years EMP is an Energy Audit. Other initiatives which have led to enhanced energy
management at the facility in recent years are enumerated as follows.
14.1.3 EMAT – Energy Monitoring System
The system was installed, to track usage of Electricity in the following areas/machines:
� Electricity at the Main meter
� Bucher Machine
� Step-lap
� Annealing Ovens
14.1.4 Sensor lighting
Installed at various areas throughout the Plant. Lights are motion controlled, they are 250 Watts v’s
450 Watts (old type) and also give out the same light strength. They are placed in areas where
people are constantly on the move in and out of:
� Maintenance offices / workshop
� Canteens
� Final Assembly area
� Over certain machines
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14.1 Best available techniques (BAT) Assessment contd:
14.1.5 Minimisation of water use
Water is not used to a significant extent in the Process. Water is employed in the Painting Process but this
water is replenished and reused where possible. The overall volume of water used is small. Projects are
continuously introduced aimed at further reducing water usage.
During 2006 the following new materials were introduced which led to reduced water usage:
� Substitution of Fixodine L refiner with Prepalene X and Additive 4977B – This is an upgraded
material, which has a longer shelf life than the material previously used. This material has a higher
stability against bath aging, thus in theory increase the amount of time our baths may be used. In turn
reduces the amount of chemical usage and thus significantly reducing water usage.
14.1.6 Minimisation of the Use of Raw Materials
A detailed inventory of materials is maintained and regular reviews of material usage are
conducted. Projects are regularly undertaken to ensure that materials use is minimised. Examples of
successful projects are listed below.
� Substitution of Novaclean A cleaner with Ridosol 525 in paint area - This is an upgraded material,
which is twice as active as the current chemical – thus the usage will reduce by 50%.
14.1.7 Minimisation of emissions
Emissions to air are minor at the facility. Temperatures are reduced in the E-Coat process leading to
lower potential for emissions and effective cleaning and pre-treatment systems are in place.
14.1.8 Waste management
Proactive waste minimisation programmes are in place throughout the facility. In 2006 the company
bought a Baler for cardboard and plastic. This led to increased recycling of cardboard 11.5Ton
(1999) to 17.7Ton (2006) and plastic 0Ton (1999) to 9.7Ton in 2006.
14.2 CONCLUSION
In conclusion a review of activities has been completed and with reference to the relevant BAT
Guidance Note, we are satisfied that BAT is being applied at the facility. As technology develops,
activities are constantly reviewed to ensure that BAT is maintained.
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15. Materials Table G.1(I) Details of Process related Raw Materials, Intermediated, Products, Etc., used or generated on the site
Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
(PO12.02) 0651-918 Alugard 16 / Hydrochloric Acid Solution for metal precipitation Yes Pungent odour Not specified Autobooth P27 - contents - Sodium Hydroxide No No No No - Sodium Carbonate No No No No
(PO26.00)
- Sodium Metasilicate No No No No No (PO30) Buffer Solution- pH 10.00 No No No No (P031) Buffer Solution - pH 4,00 No No No No (P032) Buffer Solution - pH 5,00 No No No No (P033) Buffer Solution - pH 7.00 No No No No
(PO84) Buffer Solution - pH 9,00 No No No No No
(PO39) 0651-912 Caustic Liquor 20% w/v No Negligible Not specified No No No No
(PO56.01) 0651-862 EC Neutralising Agent Not specified No No No No
EC Solvent - Contents Ethylene Glykolmonobutylether Yes, 7 No No No Diethylene Glycolmonobutylether Yes, 7 No No No Glykole Yes, 7 No No No
(PO57.01) 0651-855
Butanol Not specified Yes, 7 No No No
(PO61.00) EDTA Reagent Powder Pillows No None No No No No
(PO62.00) Macpherson Eggshell and Bases Not specified Yes, 7 No No No
0651-928 Foam block 210S Yes Odour characteristic No No No No
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Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
Colormix - White Cap - contents Acetone Yes, 7 No No No Butanone Yes, 7 No No No
(PO93.00)
Dimethyl Ether Propellant Yes Pleasant, agreeable Not specified Yes, 7 No No No
(PO94.01)0651-936 Granodine 958 Replenisher Yes Slight, acidic Not specified Yes, 4 Yes, 1,5 No No
(PO95.00) Spraymatch (Blue Cap) Yes Characteristic Not specified Yes, 7 No No No
(P112.00) Nitrogen No No odour warning Not specified No No No No
(P107.00) Macpherson Gloss and Bases Not specified Yes, 7 No No No
P111.01 (0652-050) Multi-Solve Not specified Yes, 1,4 No Yes No Novaclean 177D No No Potassium Hydroxide No No No No (P114.01) 0651-932
Sodium Hydroxide Yes Slight Not specified No No No No
Novaclean A Sodium Hydroxide (P115.01)0651-930
Non-ionic surfactants No longer in use
Novamax Accelerator 13L (P117.01)0651-938
Sodium Nitrite No None No No No No
Novamax Additive 100L (P118.01)0651-940 Sodium Hydroxide No longer in use
Novaphos Z616 CMI Phosphoric Acid No Yes, 5 No Yes (P120.01)0651-934
Nickel nitrate Yes Slight Not specified Yes, 4 Yes, 1, 5 No No
Nytro 10BN Hydrotreated Light Naphthemic Distillate Yes, 7 No No No P122.00
Clay Treated Light Naphthenic Distillate No Odourless Yes, 7 No No No
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Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
Nytro 10 GBN P123.01 (0680-001)
Hydrotreated Light Naphthemic Distillate No Odourless Yes, 7 No No No
Nytro 10 XT Hydrotreated Light Naphthenic Distillate Yes, 7 No No No P124.00 (0680-075)
2,6-ditertiary Butyl-4-Methyl Phenol No Odourless Yes, 7 No No No
P133.00 Phenolphthalein Solution Not specified No No No No
Phosphate Standard Solution Potassium Phosphate Monobasic No Yes, 5 No Yes P135.00
Demineralized Water No None No No No No Phos Ver 3 Phosphate Reagent Powder Pillows Ascorbic Acid No No No No Potassium Pyrosulfate No No No No
P136.00
Sodium Molybdate Not specified No Yes, 1 No No
P139.00 Potassium Persulfate for Phosphonate No longer in use
P147.01 Flawfinder Developer Spray Yes Characteristic Not specified No No No
Flawfinder Dye Penetrant Carbon Dioxide Aerosol Propellant No No No No Isoparaffinic Hydrocarbon Yes, 7 No No No
P148.01
White Mineral Oil Yes Characteristic Not specified Yes, 7 No No No
ROCOL Penetrating Spray Odourless Kerosene Yes, 7 No No No P149.00
Carbon Dioxide Aerosol Propellant Yes Characteristic Not specified No No No No
P150.00 Rocol RTD Liquid Yes Characteristic Not specified No No No No
P152.00 Rocol Lmtd Yes Characteristic Not specified No No No No
For
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ectio
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pose
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Conse
nt of
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uired
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se.
EPA Export 26-07-2013:02:39:10
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 44 of 47
Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
P160.00 Sigmafast Enamel Yes Characteristic Not specified NOTE IN USE
P163.01 Sodium hydroxide No Odourless No No No No
P167.01 Sulphamic acid GPR No Odourless No No No No
P169.01 Sulphuric acid 0.05mol/l (0.1N) No Odourless No No No No
Thinner 1031 Xylene,mixture of isomers Yes, 7 No No No Ethyl benzene Yes, 7 No No No n-Butanol Yes, 7 No No No
P182.01
1-Methoxy-2-propanol Not specified Yes, 7 No No No
P185.00 Machinery Enamel Not specified Urogen and Roofkote Thinners Low Boilint Point Naphtha Yes, 7 No No No Light Arom. 70-90% Yes, 7 No No No
(P188.01)0651-540
Einecs Yes Perceptible odour Not specified No No
Urogen Epithane Zinc-AL Primer (P196.01)0651-548
2-Methoxy-1-Methylethyl Acetate Yes Perceptible odour Not specified Yes, 7 No No No
(P210.01)0651-915 Hydrochloric acid Yes Pungent odour Not specified No No No No
P215.01 Nitric acid GPR Yes Pungent odour Not specified No No No No
(P224.02)0651-922 Phosclear 401 Not specified No No No No
P233.00 Metaflux 70-38 Galva-Protect Yes Characteristic NO LONGER IN USE
P236.01(0651-865) ET-Emulgator Agent Not specified No No No No
P239.01(0651-870) EC Anti-Crater Agent Not specified No No No No
P244.00 Liquified Petroleum Gas or Propane Not specified No No No No
For
insp
ectio
n pur
pose
s only
.
Conse
nt of
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r req
uired
for a
ny ot
her u
se.
EPA Export 26-07-2013:02:39:10
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 45 of 47
Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
P247.00 Methyl ethyl ketone Yes Sweetish odour -
alcohol-like Not specified Yes, 7 No No No
(P250.01) 0651-830 Aqua-EC 2000/3000 Not specified Yes, 7 No No No
P252.01 Interpon Powder Coating Not specified Yes, 7 No No No
(P253.01) 0651-875 Electrocoate Edge Protection Agent Not specified Yes, 7 No No No
(P258.00) 0651-220 Galvatect Yes Ketone solvent Not specified Yes, 7 No No No
Upol Custom Can Aerosol Acetone Yes, 7 No No No P272.00
DimethylEther Yes Characteristic Not specified Yes, 7 No No No
(P284.00)0651-915 Hydrochloric acid Yes Pungent odour Not specified No No No No
P289.00 Acetylene Yes
Poor warning properties at low concentrations -
Garlic-like Not specified No No No No
P299.01 Interpon Powder Coating Not specified No No No No
(P307.01)0651-872 Electrocoat EC-Disinfection Agent Yes Typical Not specified Yes, 7 Yes, 2 No No
(P331.00)0651-560 Urogen Gloss RAL 7033-1503 Yes Characteristic Not specified Yes, 7 No No No
(P332.00)0651-551 Urogen Gloss Clear-RAL-ALL COLOURS Yes Characteristic Not specified Yes, 7 No No No
P333.00 (0651-542) Urogen Gloss Activator (Roofkote) Yes Characteristic Not specified No No No No
P335.00 Activator for Urogen Epithane Sin-Al Primer Yes Perceptible odour Not specified No No No No
(P338.00)0651-852 Aqua-EC 3000 Pigment Paste Black Yes Typical Not specified Yes, 7 No No No
Ridosol 525
Non-ionic surfactant No No No No (P342.00) 0651-931
Anionic surfactant Yes Slight,
characteristic Not specified No No No No
For
insp
ectio
n pur
pose
s only
.
Conse
nt of
copy
right
owne
r req
uired
for a
ny ot
her u
se.
EPA Export 26-07-2013:02:39:10
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 46 of 47
Odour EU Lists I ans II (Tick and specify Group / Family Number)
Dangerous Substances Directive 76/464/EEC Groundwater Directive 80/68/EEC
Ref No. / Code Material / Substance Odourous Yes / No Description
Threshold ug/m3 List I List II +129 List I List II
Prepalene X (P356.00)0651-947
Phosphates No No valuation No Yes, 5 No Yes Additive 4977B
(P357.00)0651-948 Potassium hydroxide No None No No No No
Starter 40 (P359.00)0651-950
Sodium hydroxide No None No No No No
P360.00 Liquefied Propane Gas No Odourless No No No No
For
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ectio
n pur
pose
s only
.
Conse
nt of
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r req
uired
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EPA Export 26-07-2013:02:39:10
Additional information requirements for the EPA – regarding the new IPPCL application:
Ref: Letter – 25 June 2008 P0106-02
Page 47 of 47
16. Financial Commitment and Liabilities As previously expressed Pauwels Trafo Ireland are committed to comply with the
requirements as set out by the Integrated Pollution Prevention and Control License. We have a
designated Environmental Department and fully trained Environmental operators. We achieved
registration to the Environmental Standard ISO 14001 in 2000.The implementation of a recognized
environmental management system was in response to the growing global awareness of the
environment and the serious detrimental effect we all have on the environment in which we live. We
have also come to recognize the huge financial gain there is to implementing such a standard in
waste minimization and control coupled with higher environmental standards in the workplace.
In recognition of these gains, Pauwels wish to continually promote the growth of such
standards among its suppliers and to reward willing companies with continued custom.
As informed to the Agency in March 2005 our company was taken-over by Crompton
Greaves Ltd – an industrial conglomerate based in India. Our parent company is a very well
established firm with operations in 9 countries throughout the world. The business base for Pauwels
is strong and at least 50% of our current business coming from Renewable Energy Sector.
The financial status of the company is strong enough to guarantee funds for any environmental
restorations, which could be identified as a result of plant activities. We do not expect to suffer from
the current Economical Downturn.
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